JPS6141639B2 - - Google Patents
Info
- Publication number
- JPS6141639B2 JPS6141639B2 JP11633077A JP11633077A JPS6141639B2 JP S6141639 B2 JPS6141639 B2 JP S6141639B2 JP 11633077 A JP11633077 A JP 11633077A JP 11633077 A JP11633077 A JP 11633077A JP S6141639 B2 JPS6141639 B2 JP S6141639B2
- Authority
- JP
- Japan
- Prior art keywords
- bod
- raw water
- microorganisms
- nitrifying
- nitrifying microorganisms
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 244000005700 microbiome Species 0.000 claims description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 47
- 230000001546 nitrifying effect Effects 0.000 claims description 43
- 238000000034 method Methods 0.000 claims description 19
- 238000011282 treatment Methods 0.000 claims description 16
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- 229910052799 carbon Inorganic materials 0.000 description 10
- 239000010802 sludge Substances 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- 239000013535 sea water Substances 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 239000011345 viscous material Substances 0.000 description 3
- JVMRPSJZNHXORP-UHFFFAOYSA-N ON=O.ON=O.ON=O.N Chemical compound ON=O.ON=O.ON=O.N JVMRPSJZNHXORP-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 2
- 230000001464 adherent effect Effects 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009395 breeding Methods 0.000 description 2
- 230000001488 breeding effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000001651 autotrophic effect Effects 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
本発明は、原水中のアンモニア性窒素を好気的
条件下で亜硝酸性窒素および硝酸性窒素にする硝
化微生物を媒体表面に集殖させるに当り、媒体表
面での硝化微生物の増殖を速め、集殖期間を短縮
する汚水の硝化処理方法に関するものである。
硝化微生物によるアンモニアと亜硝酸の酸化反
応は、次の(1)、(2)式に示す通りである。
これらの反応は、硝化微生物増殖のためのエネ
ルギーを供給する。微生物細胞の実験式を
C5H7NO2し仮定するなら、硝化微生物の増殖式
は次の(3)、(4)式で示される。
上記(3)、(4)式に示されるように、自栄養性細菌
の硝化微生物は、増殖に際してアンモニア性窒素
および重炭酸、炭酸等の無機炭素を細胞合成に用
いており、その他金属、リン、無機塩類等が微量
必要となるが、有機物質を一切必要としない。し
たがつて、原水中にBOD成分を全く含んでいな
くとも、アンモニア性窒素と細胞合成に必要な無
機炭素を含んでおれば、好気的条件下で硝化処理
することが可能となるわけである。ところが、硝
化微生物はBOD分解微生物と比較すると粘性物
質の分泌が少ないためか、生物フロツク、スライ
ムの粘性が低く、媒体への付着性が悪い。
従来、硝化処理としては、ほとんどが活性汚泥
法のような生物浮遊方式による生物処理が主体で
あつた。この生物浮遊方式では、微生物の媒体へ
の付着性は問題とならないため、原水中のBOD
が5mg/以下でも硝化微生物の集殖には影響が
なかつた。
しかし、最近盛んになつてきた生物固定床方
式、すなわち散水床、浸漬床、流動床等の媒
体表面で硝化微生物を増殖させる生物処理では、
硝化処理の対象はほとんどが下水処理水、し尿処
理水等のBOD成分が5mg/以上残留する水で、
しかもBOD分解微生物が多く存在しているた
め、媒体表面への硝化微生物の集殖は問題になつ
ていなかつた。ところが、BOD5mg/以下でア
ンモニア性窒素を含む用排水についての硝化処理
では、媒体表面での硝化微生物の集殖が遅く、集
殖期間(運転開始から初期に媒体表面に硝化微生
物が付着するまでの期間)は短い時でも2ケ月、
長い時では4ケ月も要することがあつた。このよ
うにBOD5mg/以下の原水で集殖期間が長くな
るのは、今迄は植種に使用した活性汚泥中に硝化
微生物があまり含まれていなかつたためとか、無
機炭素が少なかつたためということでかたづけら
れ、硝化微生物の媒体の付着性の悪さが原因とな
つていることに気付いていなかつた。
したがつて、アンモニア性窒素の硝化を目的と
した生物固定床方式による生物処理では、アンモ
ニア性窒素を含有するがBOD5mg/以下の原水
で硝化微生物を集殖しようとすれば、従来のよう
に硝化微生物を含む活性汚泥で植種したり、リ
ン、無機炭素源、微量の金属塩等を添加したりし
ても、硝化微生物の媒体表面への付着が良くない
ために集殖期間がやたらと長くなる欠点があつ
た。
本発明は、上記生物固定床方式でBOD5mg/
以下のアンモニア性窒素を含む原水を硝化処理す
る際の従来法の欠点を除き、媒体表面への硝化微
生物の付着性を改善し、集殖期間を短縮すること
を目的とするものである。
本発明は、アンモニア性窒素を含有しBOD5
mg/以下の原水を、好気的条件下で散水床、
浸漬床、流動床等の媒体表面で硝化微生物を増
殖させる生物固定床方式によつてアンモニア性窒
素を硝酸性窒素または亜硝酸性窒素を酸化する硝
化処理において、前記硝化微生物の集殖期間中に
原水にBOD源を添加し、媒体表面にBOD分解微
生物が付着するに際して分泌する粘性物質の粘着
力を利用して付着性の悪い硝化微生物を媒体表面
に付着し易いようにし、硝化微生物の増殖を速
め、集殖期間を短縮させることを特徴とするもの
である。
ここにBODとは、JIS K0102に示されるBOD
の定義よび測定方法によるものである。また、上
記原水のBOD源の添加量は、上記BOD測定方法
で3〜20mg/、好ましくは3〜10mg/になるよ
うに調整するとよい。これは、BODを20mg/以
上にすると、媒体表面の微生物は増殖速度の大き
いBOD分解微生物が優先種になつて硝化微生物
の増殖を阻害するようになつたり、循環している
原水が汚染されたりする可能性があるためであ
る。また、BODが3mg/以下では媒体表面の
BOD分解微生物の増殖が遅くなるため、BOD分
解微生物の共存による硝化微生物付着促進の効果
が減少する。
次に本発明の実施態様を図面にもとずいて説明
する。第1図示例は硝化処理のみを行なう場合の
態様であつてBOD5mg/以下でアンモニア性窒
素を含む原水1を調整槽2に導き、ここでアルカ
リ剤3を加えてPH7〜8、好ましくはPH8〜8.5
に調整すると共にBOD源4を加える。また、原
水中に無機炭素が少ない場合には無機炭素源5を
添加する。次いでこの原水を、空気あるいは高濃
度酸素含有ガス7の曝気、溶解で好気条件に保た
れている粒状媒体を充填した硝化槽6に導くが、
集殖期間の最初に硝化微生物を植種するために硝
化微生物含有汚泥を硝化槽6に投入するとよい。
この硝化槽6内は、導入された原水1中のBOD
成分を分解する微生物とアンモニア性窒素を酸化
する硝化微生物が活動し易い条件下にあり、媒体
表面は最初付着性のよく増殖の速いBOD分解微
生物が付着し、付着性の悪い硝化微生物は、その
後BOD分解微生物の分泌する粘性物質を利用し
て付着し増殖するようになる。なお、集殖期間
中、硝化槽6からの流出水8の大部分を循環させ
て調整槽2へ戻し、流出水8中の媒体に付着でき
ずに流出した微生物と媒体との接触機会を多くす
るようにするとよい。しかし、媒体表面の微生物
量が増え、流出水中のアンモニア性窒素濃度が減
少するようになつたときにはこの循環量を減少さ
せ、また集殖期間後にはこの循環を止めてもよ
く、BOD源4の添加も不必要になる。
また第2図示例は、硝化槽6のあとに脱窒素槽
10を後続させて脱窒素処理まで行なう場合の態
様であつて、この場合、第1図示例の如く原水の
調整槽2へ新たにBOD源4を添加する代りに、
嫌気的条件下にある脱窒素槽10における脱窒素
微生物の集殖あるいは脱窒素処理のために添加す
るメタノール、グルコース、糖蜜等の有機炭素源
9の流出水中の残留分を利用することが可能であ
る。すなわち、有機炭素源9が添加され脱窒素槽
10で脱窒素されたのち流出する脱窒素処理水1
1を調整槽2に循環させ、その残留有機炭素を
BOD源として利用して硝化槽6内での硝化微生
物の集殖を促進させるのである。
以上述べたように本発明によれば、アンモニア
性窒素を含有しBOD5mg/以下の原水を好気的
条件下で生物固定床方式によつて硝化処理する方
法において、媒体表面での硝化微生物の増殖を速
め、集殖期間を短縮することができ、汚水処理を
高速かつ効果的に行なうことができるものであ
る。
次に実施例を示す。
実施例 1
BOD1.0〜3.5mg/のアンモニア含有廃水
(NH4 -N=50〜85mg/)を10倍に希釈したもの
を原水とし、10〜12mmφの砂利を高さ4mに充填
した浸漬床で硝化処理するにあたり、通水初期
に砂利表面に硝化微生物を付着させる集殖期間
中、床への流入原水にBOD源としてブドウ糖
溶液の添加を行なつた場合と行なわなかつた場合
との集殖速度を比較した結果は第1表の通りであ
つた。なお、集殖期間中の実験条件は、原水の溶
存酸素濃度37〜40mg/、PH8.5、BOD源添加後の
BOD7〜12mg/、床内上昇速度5m/h、循環
比(流出水循環水量/原水量)10とした。
The present invention speeds up the growth of nitrifying microorganisms on the surface of the medium when nitrifying microorganisms convert ammonia nitrogen in raw water into nitrite nitrogen and nitrate nitrogen under aerobic conditions. This invention relates to a method for nitrification of wastewater that shortens the breeding period. The oxidation reaction of ammonia and nitrite by nitrifying microorganisms is as shown in the following equations (1) and (2). These reactions provide energy for nitrifying microbial growth. Empirical formula for microbial cells
If C 5 H 7 NO 2 is assumed, the growth equation of nitrifying microorganisms is shown by the following equations (3) and (4). As shown in equations (3) and (4) above, nitrifying microorganisms, which are autotrophic bacteria, use ammonia nitrogen and inorganic carbon such as bicarbonate and carbonate for cell synthesis during growth, as well as other metals and phosphorus. , trace amounts of inorganic salts, etc. are required, but no organic substances are required. Therefore, even if raw water does not contain any BOD components, as long as it contains ammonia nitrogen and inorganic carbon necessary for cell synthesis, nitrification treatment can be performed under aerobic conditions. be. However, perhaps because nitrifying microorganisms secrete less viscous substances than BOD-degrading microorganisms, the viscosity of biological flocs and slime is low and their adhesion to the medium is poor. Conventionally, most nitrification treatments have been based on biological suspension methods such as the activated sludge method. With this biological suspension method, the adhesion of microorganisms to the medium is not a problem, so BOD in the raw water is
There was no effect on the population of nitrifying microorganisms even if the amount was less than 5mg/. However, the biological fixed bed method that has recently become popular, that is, biological treatment in which nitrifying microorganisms are grown on the surface of media such as sprinkled beds, immersed beds, and fluidized beds,
The targets of nitrification treatment are mostly treated sewage water, treated human waste water, etc., which contain more than 5 mg of BOD.
Moreover, since there were many BOD-degrading microorganisms present, the agglomeration of nitrifying microorganisms on the media surface was not a problem. However, in the nitrification treatment of industrial wastewater containing ammonia nitrogen with a BOD of 5mg/or less, the colony growth of nitrifying microorganisms on the media surface is slow, and the cultivation period (from the start of operation until the nitrifying microorganisms adhere to the media surface) is slow. period) is as short as two months,
At times, it could take up to four months. The reason why the cultivation period is longer in raw water with a BOD of 5mg/or less is because the activated sludge used for seeding did not contain many nitrifying microorganisms or because there was little inorganic carbon. I was not aware that the cause was poor adhesion of the nitrifying microorganisms to the medium. Therefore, in biological treatment using a biological fixed bed method for the purpose of nitrification of ammonia nitrogen, if you try to collect nitrifying microorganisms in raw water that contains ammonia nitrogen but has a BOD of 5 mg/or less, nitrification will not be possible as in the conventional method. Even if seeds are planted in activated sludge containing microorganisms or phosphorus, inorganic carbon sources, trace amounts of metal salts, etc. are added, the colonization period is excessively long because nitrifying microorganisms do not adhere well to the media surface. There was a drawback. The present invention uses the above biological fixed bed method to achieve BOD5mg/
The purpose of this method is to eliminate the drawbacks of conventional methods when nitrifying raw water containing ammonia nitrogen as described below, improve the adhesion of nitrifying microorganisms to the surface of the medium, and shorten the cultivation period. The present invention contains ammonia nitrogen and BOD5
mg/or less of raw water, under aerobic conditions, on a sprinkle bed,
In nitrification treatment in which ammonia nitrogen is oxidized to nitrate nitrogen or nitrite nitrogen by a biological fixed bed method in which nitrifying microorganisms are grown on the surface of a medium such as an immersed bed or a fluidized bed, during the cultivation period of the nitrifying microorganisms. A BOD source is added to the raw water, and the sticky force of the viscous substance secreted when BOD-degrading microorganisms adhere to the media surface is used to make it easier for nitrifying microorganisms with poor adhesion to adhere to the media surface, thereby inhibiting the growth of nitrifying microorganisms. It is characterized by speeding up the cultivation and shortening the breeding period. BOD here is BOD shown in JIS K0102.
This is due to the definition and measurement method. Further, the amount of the BOD source added to the raw water may be adjusted to 3 to 20 mg/, preferably 3 to 10 mg/, using the BOD measurement method described above. This is because when BOD is increased to 20mg/ or more, BOD-degrading microorganisms with a high growth rate become the priority species on the surface of the medium, inhibiting the growth of nitrifying microorganisms, and circulating raw water becomes contaminated. This is because there is a possibility that Also, if the BOD is less than 3mg/, the surface of the media
Since the growth of BOD-degrading microorganisms is slowed down, the effect of promoting the adhesion of nitrifying microorganisms due to the coexistence of BOD-degrading microorganisms is reduced. Next, embodiments of the present invention will be described based on the drawings. The first illustrated example is an embodiment in which only nitrification treatment is performed, and raw water 1 containing ammonia nitrogen with a BOD of 5 mg/or less is led to a regulating tank 2, where an alkaline agent 3 is added to make the pH 7-8, preferably PH 8-8. 8.5
and add BOD source 4. Furthermore, when there is little inorganic carbon in the raw water, an inorganic carbon source 5 is added. This raw water is then led to a nitrification tank 6 filled with granular media that is maintained in aerobic conditions by aeration and dissolution of air or high concentration oxygen-containing gas 7.
In order to inoculate nitrifying microorganisms at the beginning of the cultivation period, sludge containing nitrifying microorganisms may be put into the nitrification tank 6.
Inside this nitrification tank 6, the BOD of raw water 1 introduced is
The conditions are such that microorganisms that decompose components and nitrifying microorganisms that oxidize ammonia nitrogen are easily active, and BOD decomposing microorganisms that are highly adherent and grow rapidly adhere to the media surface at first, and then nitrifying microorganisms that are less adherent adhere to the media surface. It attaches and proliferates using the viscous substances secreted by BOD-degrading microorganisms. During the cultivation period, most of the outflow water 8 from the nitrification tank 6 is circulated and returned to the adjustment tank 2 to increase the chances of contact between the microorganisms in the outflow water 8 that cannot adhere to the medium and the medium. It is a good idea to do so. However, when the amount of microorganisms on the media surface increases and the ammonia nitrogen concentration in the effluent water decreases, this circulation rate can be reduced, and after the colonization period, this circulation can be stopped, resulting in BOD source 4. Addition becomes unnecessary. The second illustrated example is a mode in which a denitrification tank 10 is followed after the nitrification tank 6 to perform denitrification treatment, and in this case, as in the first illustrated example, raw water is newly added to the adjustment tank 2. Instead of adding BOD source 4,
It is possible to utilize residual amounts of organic carbon sources 9 such as methanol, glucose, and molasses in the outflow water that are added for the cultivation of denitrifying microorganisms in the denitrifying tank 10 under anaerobic conditions or for denitrifying treatment. be. That is, the denitrified water 1 that flows out after being added with the organic carbon source 9 and denitrified in the denitrifying tank 10
1 is circulated through adjustment tank 2, and the residual organic carbon is removed.
It is used as a BOD source to promote the growth of nitrifying microorganisms in the nitrification tank 6. As described above, according to the present invention, in a method for nitrifying raw water containing ammonia nitrogen and having a BOD of 5 mg/less or less by a biological fixed bed method under aerobic conditions, the growth of nitrifying microorganisms on the surface of the medium is It is possible to speed up the process, shorten the cultivation period, and perform wastewater treatment quickly and effectively. Next, examples will be shown. Example 1 A 10-fold dilution of ammonia-containing wastewater (NH 4 - N = 50-85 mg/) with a BOD of 1.0-3.5 mg/ is used as raw water, and an immersion bed is filled with gravel of 10-12 mmφ to a height of 4 m. During the nitrification treatment, nitrifying microorganisms are attached to the gravel surface at the initial stage of water flow. The results of speed comparison are shown in Table 1. The experimental conditions during the agglomeration period were: dissolved oxygen concentration in raw water 37-40mg/, pH 8.5, and after addition of BOD source.
The BOD was 7 to 12 mg/, the rate of rise in the bed was 5 m/h, and the circulation ratio (flow water circulation amount/raw water amount) was 10.
【表】
第1表から明らかなように、BOD源無添加の
原水よりBOD源を添加した原水のほうが硝化微
生物の集殖が速く、BOD源添加原水では硝化微
生物が付着して流出水中のNH4−Nが1mg/以
上になるまでに35〜40日間であるのに対して、
BOD源無添加の原水では50日以上と20〜30%も
期間が長くなつた。
実施例 2
BOD約1mg/でNH4−Nを6〜8mg/含有す
る海水を粒状活性炭による流動床方式で硝化処理
するにあたり、運転初期に活性炭表面に硝化微生
物を付着させるために、硝化微生物の少ない上記
原海水中に硝化微生物を含む汚泥(活性汚泥)を
混入し、上昇流速30m/h、循環比(流出水循環
水量/原水量)5の条件で50日間連続通水を行な
つた。しかし、それでも硝化微生物の活性炭表面
への付着が思わしくなかつたので、その後同じ通
水条件で原海水のBODが10mg/前後になるよう
にブドウ糖溶液を添加しながら30日間通水を行な
つた。その結果は第2表に示す通りであつた。[Table] As is clear from Table 1, the population of nitrifying microorganisms is faster in raw water with a BOD source added than in raw water with no BOD source added, and in the raw water with a BOD source, nitrifying microorganisms adhere to the NH 4 - It takes 35 to 40 days for N to reach 1 mg/ or more, whereas
With raw water without BOD source additives, the period was 20-30% longer, over 50 days. Example 2 When nitrifying seawater containing approximately 1 mg BOD and 6 to 8 mg/NH 4 -N using a fluidized bed method using granular activated carbon, nitrifying microorganisms were added to the surface of the activated carbon at the beginning of operation. Sludge containing nitrifying microorganisms (activated sludge) was mixed into the small amount of raw seawater mentioned above, and water was continuously passed through the seawater for 50 days under conditions of an upward flow rate of 30 m/h and a circulation ratio (effluent circulating water volume/raw water volume) of 5. However, the adhesion of nitrifying microorganisms to the surface of the activated carbon remained unsatisfactory, so water flow was continued for 30 days under the same water flow conditions while adding a glucose solution so that the BOD of raw seawater was approximately 10 mg/kg. The results were as shown in Table 2.
【表】
第2表から明らかなように、BOD源無添加の
期間中は、通水開始から50日経過してもNH4−N
は2.5mg/しか硝化されなかつたが、BOD源とし
てブドウ糖溶液を添加したところ、30日間で2.5
mg/から7.2mg/と190%も硝化されるNH4−N
の量が増加した。このように、硝化微生物の集殖
期間中にBODの低いNH4−N含有原水にBOD源
を添加することによつて、硝化微生物の媒体への
付着を速めることができる。[Table] As is clear from Table 2, during the period without BOD source addition, even after 50 days have passed since the start of water flow, NH 4 -N
However, when glucose solution was added as a BOD source, 2.5 mg/g was nitrified in 30 days.
NH 4 −N nitrified by 190% from mg/ to 7.2 mg/
The amount of has increased. In this way, by adding a BOD source to the NH4 -N containing raw water with low BOD during the cultivation period of nitrifying microorganisms, it is possible to accelerate the attachment of nitrifying microorganisms to the medium.
第1図および第2図は、それぞれ本発明の実施
態様を示す系統説明図である。
1……原水、2……調整槽、4……BOD源、
6……硝化槽、8……流出水、9……有機炭素
源、10……脱窒素槽、11……脱窒素処理水。
FIG. 1 and FIG. 2 are system explanatory diagrams showing embodiments of the present invention, respectively. 1...Raw water, 2...Adjustment tank, 4...BOD source,
6... Nitrification tank, 8... Runoff water, 9... Organic carbon source, 10... Denitrification tank, 11... Denitrification treated water.
Claims (1)
下の原水を好気的条件下で媒体表面で硝化微生物
を増殖させる生物固定床方式によつて硝化処理す
る方法において、前記硝化微生物の集殖期間中に
原水にBOD源を添加することを特徴とする硝化
処理方法。 2 前記原水に添加するBOD源の添加率を3〜
20mg/とする特許請求の範囲第1項記載の硝化
処理方法。 3 前記硝化処理の流出水を前記硝化微生物の集
殖期間中原水中に循環させる特許請求の範囲第1
項又は第2項記載の硝化処理方法。 4 前記原水に添加するBOD源として、後続す
る嫌気的条件下にある脱窒素工程流出水を利用す
る特許請求の範囲第1項又は第2項記載の硝化処
理方法。[Scope of Claims] 1. A method for nitrifying raw water containing ammonia nitrogen and having a BOD of 5 mg/less or less by a biological fixed bed method in which nitrifying microorganisms are grown on the surface of a medium under aerobic conditions. A nitrification treatment method characterized by adding a BOD source to raw water during the cultivation period. 2 The addition rate of the BOD source added to the raw water is 3~
The nitrification treatment method according to claim 1, wherein the amount is 20mg/. 3. Claim 1, wherein the effluent from the nitrification treatment is circulated into the raw water during the cultivation period of the nitrifying microorganisms.
The nitrification treatment method according to item 1 or 2. 4. The nitrification treatment method according to claim 1 or 2, wherein the subsequent denitrification step effluent under anaerobic conditions is used as a BOD source to be added to the raw water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11633077A JPS5450146A (en) | 1977-09-28 | 1977-09-28 | Treatment of nitrification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11633077A JPS5450146A (en) | 1977-09-28 | 1977-09-28 | Treatment of nitrification |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5450146A JPS5450146A (en) | 1979-04-19 |
| JPS6141639B2 true JPS6141639B2 (en) | 1986-09-16 |
Family
ID=14684292
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11633077A Granted JPS5450146A (en) | 1977-09-28 | 1977-09-28 | Treatment of nitrification |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5450146A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5626588A (en) * | 1979-08-07 | 1981-03-14 | Ebara Infilco Co Ltd | Disposal method for organic waste water |
| JP2012005911A (en) * | 2010-06-22 | 2012-01-12 | N Ii T Kk | Nitrification treatment method of waste liquid |
-
1977
- 1977-09-28 JP JP11633077A patent/JPS5450146A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5450146A (en) | 1979-04-19 |
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